Mixture of n-Butyl ether + Heptane + Cyclohexane

Excel

n-Butyl ether

Name
n-Butyl ether
InChI
InChI=1S/C8H18O/c1-3-5-7-9-8-6-4-2/h3-8H2,1-2H3
InChI Key
DURPTKYDGMDSBL-UHFFFAOYSA-N
Formula
C8H18O
SMILES
CCCCOCCCC
Mol. Weight (g/mol)
130.23
CAS
142-96-1

Heptane

Name
Heptane
InChI
InChI=1S/C7H16/c1-3-5-7-6-4-2/h3-7H2,1-2H3
InChI Key
IMNFDUFMRHMDMM-UHFFFAOYSA-N
Formula
C7H16
SMILES
CCCCCCC
Mol. Weight (g/mol)
100.20
CAS
142-82-5

Cyclohexane

Name
Cyclohexane
InChI
InChI=1S/C6H12/c1-2-4-6-5-3-1/h1-6H2
InChI Key
XDTMQSROBMDMFD-UHFFFAOYSA-N
Formula
C6H12
SMILES
C1CCCCC1
Mol. Weight (g/mol)
84.16
CAS
110-82-7
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Datasets

  1. Pvap - Vapor or sublimation pressure, kPa (2)

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Fixed Measured
Mole fraction of n-Butyl ether (1) - Liquid Mole fraction of Cyclohexane (3) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 0.0000 12.33
0.0000 0.2808 16.04
0.0000 0.6836 20.99
0.0000 1.0000 24.62
0.0001 1.0000 24.61
0.0258 0.2736 15.65
0.0271 0.6651 20.45
0.0473 0.2675 15.34
0.0489 0.6501 20.04
0.0867 0.2565 14.76
0.1016 0.6141 19.02
0.1335 0.2434 14.09
0.1475 0.3486 15.29
0.1482 0.5823 18.13
0.1522 0.5033 17.18
0.1624 0.3839 15.56
0.1680 0.4517 16.39
0.1743 0.2319 13.51
0.1773 0.4190 15.84
0.1842 0.3987 15.60
0.1920 0.4535 16.11
0.1990 0.3504 14.82
0.1991 0.5475 17.15
0.2064 0.4877 16.36
0.2134 0.3035 14.08
0.2221 0.5246 16.64
0.2228 0.2183 12.81
0.2294 0.2512 13.25
0.2374 0.5607 16.91
0.2450 0.2006 12.46
0.2506 0.5123 16.17
0.2525 0.5963 17.17
0.2583 0.1571 11.76
0.2662 0.6287 17.39
0.2685 0.2055 12.16
0.2725 0.1106 11.02
0.2809 0.6634 17.64
0.2882 0.0595 10.20
0.2899 0.6847 17.79
0.2940 0.0403 9.89
0.2968 0.4808 15.28
0.2975 0.7025 17.90
0.3064 0.0000 9.25
0.3158 0.1922 11.49
0.3326 0.1511 10.83
0.3465 0.4980 15.05
0.3476 0.4460 14.31
0.3611 0.1795 10.86
0.3656 0.1661 10.67
0.3808 0.4482 14.09
0.3960 0.4129 13.39
0.4001 0.1817 10.51
0.4103 0.1657 10.18
0.4153 0.3983 13.12
0.4348 0.1975 10.47
0.4468 0.3782 12.43
0.4508 0.3468 12.12
0.4634 0.1507 9.44
0.4718 0.2143 10.16
0.4824 0.3011 11.23
0.4967 0.3441 11.48
0.5044 0.2290 10.00
0.5137 0.2556 10.34
0.5408 0.2455 9.81
0.5533 0.1983 9.21
0.5799 0.2633 9.60
0.5852 0.1522 8.31
0.6077 0.2758 9.46
0.6172 0.1057 7.41
0.6465 0.2935 9.24
0.6477 0.0615 6.55
0.6663 0.0346 6.02
0.6700 0.3041 9.12
0.6878 0.3122 9.10
0.6902 0.0000 5.35
1.0000 0.0000 2.04
1.0000 0.0000 2.06
1.0000 0.0000 2.04

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Fixed Measured
Mole fraction of n-Butyl ether (1) - Liquid Mole fraction of Cyclohexane (3) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 0.0000 12.33
0.0000 0.2808 16.04
0.0000 0.6836 20.99
0.0000 1.0000 24.62
0.0001 1.0000 24.61
0.0258 0.2736 15.65
0.0271 0.6651 20.45
0.0473 0.2675 15.34
0.0489 0.6501 20.04
0.0867 0.2565 14.76
0.1016 0.6141 19.02
0.1335 0.2434 14.09
0.1475 0.3486 15.29
0.1482 0.5823 18.13
0.1522 0.5033 17.18
0.1624 0.3839 15.56
0.1680 0.4517 16.39
0.1743 0.2319 13.51
0.1773 0.4190 15.84
0.1842 0.3987 15.60
0.1920 0.4535 16.11
0.1990 0.3504 14.82
0.1991 0.5475 17.15
0.2064 0.4877 16.36
0.2134 0.3035 14.08
0.2221 0.5246 16.64
0.2228 0.2183 12.81
0.2294 0.2512 13.25
0.2374 0.5607 16.91
0.2450 0.2006 12.46
0.2506 0.5123 16.17
0.2525 0.5963 17.17
0.2583 0.1571 11.76
0.2662 0.6287 17.39
0.2685 0.2055 12.16
0.2725 0.1106 11.02
0.2809 0.6634 17.64
0.2882 0.0595 10.20
0.2899 0.6847 17.79
0.2940 0.0403 9.89
0.2968 0.4808 15.28
0.2975 0.7025 17.90
0.3064 0.0000 9.25
0.3158 0.1922 11.49
0.3326 0.1511 10.83
0.3465 0.4980 15.05
0.3476 0.4460 14.31
0.3611 0.1795 10.86
0.3656 0.1661 10.67
0.3808 0.4482 14.09
0.3960 0.4129 13.39
0.4001 0.1817 10.51
0.4103 0.1657 10.18
0.4153 0.3983 13.12
0.4348 0.1975 10.47
0.4468 0.3782 12.43
0.4508 0.3468 12.12
0.4634 0.1507 9.44
0.4718 0.2143 10.16
0.4824 0.3011 11.23
0.4967 0.3441 11.48
0.5044 0.2290 10.00
0.5137 0.2556 10.34
0.5408 0.2455 9.81
0.5533 0.1983 9.21
0.5799 0.2633 9.60
0.5852 0.1522 8.31
0.6077 0.2758 9.46
0.6172 0.1057 7.41
0.6465 0.2935 9.24
0.6477 0.0615 6.55
0.6663 0.0346 6.02
0.6700 0.3041 9.12
0.6878 0.3122 9.10
0.6902 0.0000 5.35
1.0000 0.0000 2.04
1.0000 0.0000 2.06
1.0000 0.0000 2.04

Sources